Process characteristics of clinker and cement production · Cement plant with rotary kiln, preheater tower and raw material grinding . Cement production process: Thermal energy demand

Process characteristics of clinker and

cement production

Johannes Ruppert [email protected]

CLUSTER Meeting, Hamburg, 26.10.2017

Cement production and concrete as building material

The properties of concrete

make it a primary building

material where reliability and

durability are required.

Depending on the application

~ 300 kg cement are used for

1 m3 of concrete.

The cement industry emits

~ 7% of global anthropogenic

CO2 emissions. China >50%.

Cement plant with rotary kiln, preheater tower and

raw material grinding

Cement production process:

Thermal energy demand and CO2 emissions

30% fuel emissions

thermal energy prod. process emissions from calcination of limestone 60%

10% electric power

consumption, indirect

emissions

Limestone Quarry

Clinker

Cement

Cement Mills

Raw Mill

Calcination

Cement

Constituents

Crusher Fan

Rotary Kiln

Pre

heate

r

Cooler

Filter

Cooler

Drying

Clinker

burning 950°C

1450°C

Drying

Continuous high temperature process in the cement

industry: Calcination and cement clinker burning

Calcination of raw material

CaCO3 => CaO + CO2

Process emissions of raw material:

= 0.54 t CO2/t clinker

Endotherm reaction at 950 °C

ca. 1700 MJ/t clinker

≈ 50% of energy

Cement clinker burning at 1450 °C

formation of hydraulic

properties of clinker

Thermal energy requirement:

ca. 3510 MJ/t clinker

(CSI GNR-2014)

Electrical energy requirement:

ca. 110 kWh/t cement (VDZ)

View into a rotary kiln

Technology for a better society

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CLUSTER Meeting, Hamburg, 26 October 2017

Johannes Ruppert

VDZ gGmbH - Research Institute of the Cement industry

CEMCAP – first experimental results and conclusions

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CEMCAP Consortium Cement Producers Italcementi, IT Norcem, NO HeidelbergCement, DE

Technology Providers GE Carbon Capture (GE-DE), DE GE Power Sweden (GE-SE), SE IKN, DE ThyssenKrupp Industrial Solutions, DE

Research Partners SINTEF Energy Research, NO ECRA (European Cement Research Academy), DE TNO, NL EHTZ, CH University of Stuttgart, DE Politecnico di Milano, IT CSIC, ES VDZ, DE

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CEMCAP ambition

• CEMCAP will deliver strategic conclusions for how to progress CO2 capture from cement plants from pilot-scale testing to demonstration

• Recommendations will be given for different scenarios (i.e. different types of cement plants at different locations in Europe)

• Focus is on retrofit – very few new cement plants are foreseen to be built in Europe

CEMCAP

• CEMCAP oxyfuel results will be directly exploited in the ECRA CCS project

• Ca-looping results in H2020 CLEANKER project

• Exchanges with LILAC project: Direct separation technology


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Oxyfuel capture

Experimental CEMCAP research


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Oxyfuel cement burner tests

Result from the SINTEF CFD simulation of the oxy-fuel case tested in the second campaign showing streamlines coloured by temperature.

Measurements of incident total heat flux to the furnace wall during second test campaign.

Oxyfuel burner design by ThyssenKrupp for cement plant operating conditions

Oxyfuel burner testing at IFK, University of Stuttgart


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• Purpose is experimental investigation of suspension calcination under industrially relevant oxy-fuel conditions

• Aim is to verify sufficient calcination of the raw material before its entering into the rotary kiln

• Experimental work is concluded, final analysis ongoing

Calciner technology for oxyfuel capture


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Hot commissioning of the oxyfuel clinker cooler and first oxyfuel clinker samples

Oxyfuel clinker cooler – designed, built, tested

Clinker cooler prototype and recirculation system installation at HeidelbergCement in Hannover

Clinker analysis is ongoing


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• Considerably high false air ingress through the cold clinker discharge system outlet.

• No leakages of CO2–rich gas occurred during the trials.

• Cooling gas recirculation contributed to a phenomenon of moisture enrichment.

• The clinker microstructure of the clinker samples indicate fast cooling .

• Cooling rate was enhanced by the extraction of finer clinker granules from the kiln and high false air ingress.

WP 9 – Experimental results


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WP9 researchers concluded that…

• … if high water contents in the cooling medium prove to affect product quality, special attention shall be given to the design of the condenser, whose installation in future oxyfuel cement plants has been already envisaged by ECRA.

• … cold clinker discharge system shall get special attention regarding minimisation of false air in-leakage in industrial scale projects.

WP 9 – Relevant findings for the industry

• … equipment sealing proved to be effective at pilot scale. The use of similar sealing technology in industrial scale shall be regarded with caution:

1) operation conditions are more severe in industrial scale.

2) sealing’s durability and efficiency over time were not assessed during the experiment.


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Post combustion capture

Experimental CEMCAP research


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• ETHZ has simulated and adapted the CAP system to different cement-plant flue gases;

• New rate-based model was developed and used to validate full-scale CAP simulations for cement plants. Upcoming work: CAP optimization

• The Absorber and Direct Contact Cooler (DCC) units were tested under cement-like conditions at GE Power Sweden, Water wash section will be tested later in 2017

Chilled ammonia for cement plant CO2 capture

DCC pilot at GE Power Sweden

CAP process flowsheet


16 Membrane-assisted CO2 liquefaction

• End-of-pipe technology

(requires De-SOx, De-NOx, dehydration)

• No fuel input, only power

• Membrane testing: TNO

• Liquefaction testing: SINTEF


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• Tail-end CO2 capture: tests at 200 kW Ca-looping CFB test facility at IFK/Stuttgart University

Calcium looping for cement plants

Experimental results on CaL CO2 capture efficency versus equilibirum CO2 capture (IFK/USTUTT)

• Entrained-flow (integrated) Ca-looping: tests at CSIC

• Process simulations/sizing of full-scale Ca-looping conducted alongside exp work (Politecnico di Milano)

• "Spin-off project" H2020 CLEANKER

Air/CO2/H2O

ENT

RA

INED

CA

RB

ON

AT

OR

T1

T5

T4

T3

T2

T6

T7

Gas toanalyzer 1

Gas toanalyzer 2

Sorbent/Air

Gas/Solids

2,4 m

3,0 m

Experimental setup at CSIC


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Analytical CEMCAP research


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• For consistent comparative assessment of capture technologies for cement plants

• Provides information relevant for experimental and simulation work

CEMCAP framework document: ready for use!

• Defines:

• A reference cement clinker production line

• Specs for standard process units

• Utilities description, cost and climate impact

• Extent of capture and CO2 specs

• Economic parameters

• Key performance parameters

Download from www.sintef.no/cemcap/results

http://www.sintef.no/cemcap/results


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• Concluded and avaialble on the CEMCAP website:

• A BAT reference cement plant report, relying on the CEMCAP framework

• A cement plant reference case with MEA (also poster/paper at GHGT13)

• Work in progress, not published:

• Process simulations with comparsion of CO2 capture

• Costing methodology

Comparative capture process analysis (benchmarking)

• Remaining work:

• Final process simulations of all capture technologies

• Retrofitability study

• Final techno-economic comparison

VDZ clinker production process model


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Process analysis example: Oxyfuel modelling

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Purpose: Optimization of the oxyfuel clinker burning process based on process modeling verified by prototype results

Oxyfuel principle: Air is replaced by recirculated CO2 in the plant, to enable capture of highly concentrated CO2

Oxyfuel research in CEMCAP is closely connected to the ECRA CCS project

1. Pre-calciner, 2. burner and 3. clinker cooler tested in CEMCAP


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Oxyfuel modelling: CPU electrical energy demand depending on air in leakage

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Possibilities for power generation by fuel feed variation


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Effect of false air ingress variation: +4% false air = +13% CPU power demand

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Fals air ingress 4% 6% 8%

Feed purity (dry), mol% 88.2 84.3 80.7

CO2 product purity, mol% 97.6 97.5 97.2

CO2 capture ratio, % 90 90 90

CPU power, kWh/t CO2 167 173 189

Effect of increased fuel input for Waste Heat Recovery (WHR)

• Fuel feed variation

– Increase in fuel thermal energy input of 2150 kW

– The electricity output from the ORC increased by 450 kW

– This represents an high ORC efficiency of 21 %, however lower than power plants

Modelling results and relevant findings for the industry


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• Cement-production post-capture CO2 management routes investigated in CEMCAP:

1. CCS: Geological sequestration: option to be defined (TNO)

2. CCS: Mineralization to MgCO3 (ETH Zurich)

3. CCU: CO2 hydrogenation to ethanol (TNO)

4. CCU: CO2 polymerization to Poly(propylene carbonate) (TNO)

5. CCU: food-grade CO2 (TNO)

• Product fact sheets for different CCU routes are being prepared and will be published in October

Post capture CO2 management

(what to do with the captured CO2 if you are in the cement industry?)


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• Oxyfuel clinker cooler experiment in HeidelbergCement plant Hannover until 3/2017

• Oxyfuel calciner and burner experiments at University of Stuttgart: 8/2017, 12/2017

Oxyfuel experimental workpackages are concluding their work in 2017


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Carbon Capture Technologies in the Cement Industry 2nd ECRA/CEMCAP Workshop, Düsseldorf, 6-7 November

• 90 participants, 50% industry

• Poster session: Draft conclusions from CEMCAP research work packages

Presentations and discussions

• Oxyfuel clinker cooler technology and experiment film

• Calcium looping capture in the cement industry

• Geological CO2 storage

• Membrane-assisted CO2 liquefaction

• Commercial use of captured CO2 and CCU options for the cement industry

• Direct separation technology for capturing process CO2 emissions, H2020 project LEILAC

• The full-scale CCS project at Norcem Brevik: Can it be realized?

• EU CCS policy and possibilities for R&I funding

https://ecra-online.org/seminars-and-events/overview/









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• Public deliverables are uploaded to our website:

www.sintef.no/cemcap/results

• CEMCAP Framework document

• Oxyfuel clinker cooler film

• On twitter (@cemcap_co2) we announce newly published deliverabes, newsletters, blogs and other CEMCAP-related info and events

• Subscribe to newsletters: send an e-mail to [email protected]

• Final CEMCAP/ECRA workshop in Brussels mid-October 2018 (before GHGT-14)

To follow CEMCAP:

http://www.sintef.no/cemcap/resutls

mailto:[email protected]


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Acknowledgements

This project has received funding from the European Union's Horizon 2020 research and innovation programme under grant agreement no 641185

This work was supported by the Swiss State Secretariat for Education, Research and Innovation (SERI) under contract number 15.0160

www.sintef.no/cemcap

Twitter: @CEMCAP_CO2

Newsletter subscription, inquiries: [email protected]

http://www.sintef.no/cemcap

mailto:[email protected]

Documents

Process characteristics of clinker and cement production · Cement plant with rotary kiln, preheater tower and raw material grinding . Cement production process: Thermal energy demand